# US 10,245,611 B2 · Slurry distribution system and method > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 10,245,611 B2 - Document ID: US10245611B2 - Status: Granted - Kind: B2 - Application number: 15/445,794 - Filed: 2017-02-28 - Published: 2017-06-15 - Granted: 2019-04-02 - Earliest claimed: 2010-12-30 - Assignees: United States Gypsum Company - Applicants: United States Gypsum Company - Inventors: Alfred C. Li; Christopher C. Lee; Christopher Nelson; Cesar Chan; James Wittbold; Weixin D. Song - Web page: https://patentgrep.com/patent/US10245611B2 ## CPC - B05C 5/0254: {Coating heads with slot-shaped outlet (B05C5/0283 takes precedence)} - B05C 5/0262: {adjustable in width, i.e. having lips movable relative to each other in order to modify the slot width, e.g. to close it} - B05C 11/10: Storage, supply or control of liquid or other fluent material; Recovery of excess liquid or other fluent material {(B05C1/0813, B05C5/0225, B05C17/002 and B05C19/06 take precedence)} - B05D 1/28: performed by transfer from the surfaces of elements carrying the liquid or other fluent material, e.g. brushes, pads, rollers - B28B 19/0092: {to webs, sheets or the like, e.g. of paper, cardboard} - B05C: APPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL (spraying apparatus, atomising apparatus, nozzles B05B; plant for applying liquids or other fluent materials to objects by electrostatic spraying B05B5/08) - B05D: PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL (conveying articles or workpieces through baths of liquid B65G, e.g. B65G49/02) - B28B: SHAPING CLAY OR OTHER CERAMIC COMPOSITIONS; SHAPING SLAG; SHAPING MIXTURES CONTAINING CEMENTITIOUS MATERIAL, e.g. PLASTER (foundry moulding B22C; working stone or stone-like material B28D; shaping of substances in a plastic state, in general B29C; making layered products not composed wholly of these substances B32B) ## Abstract A slurry distributor for use in a continuous manufacturing process includes an inlet opening and a shaped duct adapted to receive a flow of slurry provided at the inlet opening. The shaped duct has a parabolic guide surface adapted to redirect the flow of slurry. An outlet opening in fluid communication with the shaped duct is adapted to discharge the flow of slurry from the slurry distributor. ## Claims ### Claim 1 A slurry distributor for use in a continuous manufacturing process, the slurry distributor comprising: an entry segment defining an inlet opening; a shaped duct in fluid communication with the inlet opening; and an outlet defining an outlet opening in fluid communication with the shaped duct; wherein the shaped duct includes a parabolic guide surface adapted to redirect a flow of slurry moving from the inlet opening through the shaped duct to the outlet opening from an inlet direction to an outlet direction, and wherein a cross-sectional flow area of the outlet opening is in a range from greater than to 400% of a cross-sectional flow area of the inlet opening. ### Claim 2 (depends on 1) The slurry distributor of claim 1, wherein the width of the outlet opening extends along a transverse axis and a substantial portion of the parabolic guide surface is aligned with the width of the outlet opening along the transverse axis. ### Claim 3 (depends on 1) The slurry distributor of claim 1, wherein the shaped duct has a generally rectangular cross section and a generally curved outer wall that defines the parabolic guide surface such that a flow of slurry entering the slurry distributor through the inlet opening is redirected by a change in direction angle before exiting through the outlet opening. ### Claim 4 (depends on 3) The slurry distributor of claim 3, wherein the entry segment is generally cylindrical and further comprising a round-to-rectangular cross section transition segment disposed between the entry segment and the shaped duct. ### Claim 5 (depends on 1) The slurry distributor of claim 1, wherein the parabolic guide surface is at least partially defined by an outer curved wall of the duct. ### Claim 6 (depends on 1) The slurry distributor of claim 1, wherein the duct is further defined by an inner slanted wall extending at an obtuse angle relative to an outlet plane defined by the outlet opening. ### Claim 7 (depends on 1) The slurry distributor of claim 1, wherein the flow of slurry is redirected from an inlet flow direction to an outlet flow direction by a change in direction angle within a range of about forty-five degrees to about one hundred fifty degrees. ### Claim 8 (depends on 1) The slurry distributor of claim 1, further comprising: a profiling system adapted to locally vary the shape of the opening of the outlet opening. ### Claim 9 (depends on 1) The slurry distributor of claim 1, further comprising a second inlet opening in fluid communication with the shaped duct. ### Claim 10 (depends on 1) The slurry distributor of claim 1, wherein the duct has a cross sectional flow area that increases in a direction from the inlet opening toward the outlet opening. ### Claim 11 A method for providing a slurry to an advancing web, the method comprising: passing a flow of aqueous gypsum slurry in an inlet flow direction through an inlet of a slurry distributor having a shaped duct with a parabolic guide surface such that the parabolic guide surface redirects the flow of slurry from the inlet flow direction to an outlet flow direction toward an outlet opening of the slurry distributor; and discharging the flow of the aqueous gypsum slurry from the outlet in the outlet flow direction upon an advancing web of cover sheet material, wherein a cross-sectional flow area of the outlet is in a range from greater than to 400% of a cross-sectional flow area of the inlet, and wherein the outlet flow direction of the flow of the aqueous gypsum slurry discharging from the outlet is substantially parallel to a line of travel of the advancing web of cover sheet material. ### Claim 12 (depends on 11) The method of claim 11, wherein the parabolic guide surface redirects the flow of slurry from the inlet flow direction to the outlet flow direction by a change in direction angle within a range of about forty-five degrees to about one hundred fifty degrees. ### Claim 13 (depends on 11) The method of claim 11, wherein the parabolic guide surface redirects the flow of slurry from the inlet flow direction to the outlet flow direction by a change in direction angle within a range of about eighty degrees to about one hundred degrees. ### Claim 14 (depends on 11) The method of claim 11, further comprising passing at least one additional flow of slurry through the shaped duct through a secondary inlet of the shaped duct. ### Claim 15 (depends on 11) The method of claim 11, further comprising: adjusting the shape of the outlet opening to vary the flow of aqueous gypsum slurry discharging through the outlet.